US11840667B2ActiveUtilityA1

Depolymerization of recovered plastic materials

84
Assignee: DENG SHUGUANGPriority: Jul 7, 2021Filed: Jul 7, 2022Granted: Dec 12, 2023
Est. expiryJul 7, 2041(~15 yrs left)· nominal 20-yr term from priority
C10G 1/10B01D 3/145B01D 53/229B01J 6/008C08J 11/08C10G 1/002C08J 2323/06C10G 2300/1003Y02W30/62C08J 11/14C08J 11/22C08J 11/24B01J 31/0298B01J 31/0284
84
PatentIndex Score
2
Cited by
80
References
18
Claims

Abstract

Described herein are systems and methods for the depolymerization of polyethylene-based plastics. In one embodiment, a method is disclosed that comprises combining a polyethylene-based plastic with a solvent in a reactor to generate a plastic solvent mixture, heating the plastic solvent mixture in the reactor, and fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product. In another embodiment, a system is disclosed that comprises a solvent, and a reactor configured to receive the polyethylene-based plastic and the solvent and convert the polyethylene-based plastic into a gas phase product, a solid phase product, and a liquid phase product, the reactor being configured to operate at a temperature greater than 275° C. and at a pressure greater than 2 megapascals.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
       1. A method for depolymerizing a polyethylene-based plastic, the method comprising:
 combining the polyethylene-based plastic with a solvent in a reactor to generate a plastic solvent mixture; 
 heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C. for no less than 70 minutes and no greater than 120 minutes; and 
 fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product wherein the plastic solvent mixture is further combined with an ionic liquid catalyst prior to heating with. 
 
     
     
       2. The method according to  claim 1 , wherein the solvent comprises at least one of water, methanol, ethanol, butanol, isopropyl alcohol, or acetone. 
     
     
       3. The method according to  claim 2 , wherein the solvent comprises acetone. 
     
     
       4. The method according to  claim 1 , wherein the ionic liquid catalyst comprises 1-butyl-3-methylimidazolium, bis[(perfluoroethyl)sulfonyl]-imide ([BMIM][PF2]), 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM][BF4]), 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM][PF6]), or combinations thereof. 
     
     
       5. The method according to  claim 1 , wherein the heating is performed at about 300° C. to 360° C. 
     
     
       6. The method according to  claim 5 , wherein the heating is performed between about 340° C. to 360° C. 
     
     
       7. The method according to  claim 1 , wherein the heating is performed at a pressure of about 2 megapascals to about 20 megapascals. 
     
     
       8. The method according to  claim 7 , wherein the heating is performed at a pressure of about 8 megapascals to about 11 megapascals. 
     
     
       9. The method according to  claim 1 , wherein the heating is performed for about 80 minutes to about 100 minutes. 
     
     
       10. The method according to  claim 1 , wherein the plastic solvent mixture is combined in a weight/volume ratio of about 1 gram plastic:6 mL solvent to about 1 gram plastic:20 mL solvent. 
     
     
       11. The method according to  claim 1 , further comprising separating the gas phase product and the liquid phase product using a combined membrane and adsorption process. 
     
     
       12. The method according to  claim 1 , wherein at least 60% of the polyethylene-based plastic is converted into the gas phase product and the liquid phase product. 
     
     
       13. The method according to  claim 1 , wherein at least 30% of the polyethylene-based plastic is converted into the liquid phase product. 
     
     
       14. The method according to  claim 1 , wherein the liquid phase product has an oxygen/carbon ratio of about 0.01 to about 0.70. 
     
     
       15. The method according to  claim 1 , wherein the liquid phase product has a hydrogen/carbon ratio of about 1.4 to about 2.0. 
     
     
       16. The method according to  claim 1 , wherein the liquid phase product has a high heat value of about 35 MJ/kg to about 45 MJ/kg. 
     
     
       17. A method for depolymerizing a polyethylene-based plastic, the method comprising:
 combining the polyethylene-based plastic with a solvent comprising acetone in a reactor to generate a plastic solvent mixture; 
 heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C., at a pressure greater than 2 megapascals, and for no less than 70 minutes and no greater than 120 minutes; 
 fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product; and 
 
       separating the gas phase product and the liquid phase product using a combined membrane and adsorption process. 
     
     
       18. A method for depolymerizing a polyethylene-based plastic, the method comprising:
 combining the polyethylene-based plastic with a solvent comprising acetone in a reactor to generate a plastic solvent mixture; 
 heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C. for no less than 70 minutes and no greater than 120 minutes; and 
 fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product.

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